CN1250681A - Bipolar film and its preparing process - Google Patents
Bipolar film and its preparing process Download PDFInfo
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- CN1250681A CN1250681A CN 99125066 CN99125066A CN1250681A CN 1250681 A CN1250681 A CN 1250681A CN 99125066 CN99125066 CN 99125066 CN 99125066 A CN99125066 A CN 99125066A CN 1250681 A CN1250681 A CN 1250681A
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Abstract
This invented bipolar membrane is composed of anion exchange layer, cation exchange layer and intermediate layer. The base materials for the above three layers all are chloromethylated polysulfone whose chloromethyl group content is 1.1-3.5 mg equivalent/g. The intermediate layer is of the structure containing quaternary ammonium type strong alkaline group, non-quaternary ammonium type weak alkaline group and sulfonic acid type group. This invented membrane making procedure is simpler than prior art method, good in stability of tightly combined anion and cation two layer membranes, and has "intermediate layer" further super-thinned so as to make the bipolar membrane have long period operating stability.
Description
The invention belongs to technical field of chemical engineering, particularly to the preparation method's of material, membrane structure and the film of sandwich construction bipolar membrane improvement.
Bipolar membrane can be used for rectification, improve desalination processes, simulate some biomembrane and in electrodialytic process dissociate water salting liquid is transformed corresponding bronsted lowry acids and bases bronsted lowry, wherein last specific character is even more important.Multiple soluble-salt can utilize bipolar membrane electrodialysis water decomposition device to change into commercial useful bronsted lowry acids and bases bronsted lowry.
Friette finds bipolar membrane water decomposition phenomenon from the fifties, and the technology of preparing of bipolar membrane has experienced evolution slowly.From initial simple " laminated-type " structure, " adhesion type " structure, to " monolithic type " at the beginning of the eighties, up to the sandwich construction that has " intermediate layer " that the later stage eighties occurs, bipolar membrane voltage is progressively reduced, and has reached the practicability requirement.
" laminated-type " be with homogeneous phase or out-phase anion-exchange membrane and cation-exchange membrane through heating pressurize bipolar membrane (United States Patent (USP) 2829095, United States Patent (USP) 3372101 and BP 1038777); " adhesion type " is to get bipolar membrane (United States Patent (USP) 3388080 and United States Patent (USP) 3654125) with polyion sticky matter bonding anion-exchange membrane and cation-exchange membrane; " monolithic type " is the bipolar membrane (United States Patent (USP) 4024043, United States Patent (USP) 4057481 and United States Patent (USP) 4140815) of introducing cation and anion exchange groups same basement membrane both sides respectively.The bipolar membrane phase boundary potential of method for preparing falls very big, can't work under high current density.
The sandwich construction bipolar membrane that has " intermediate layer " then shows high mechanical strength, high differential permeability, low resistance and low voltage drop (United States Patent (USP) 4116889 under high current density, Deutsche Bundespatent 4026154, European patent 143582 and United States Patent (USP) 4766161).The sandwich construction bipolar membrane of this having " intermediate layer " generally needed for three steps just can make with The tape casting at least.The key of decision bipolar membrane performance quality is exactly to control the thickness and the chemical constitution thereof in the intermediate layer between the yin, yang rete.
The sandwich construction bipolar membrane (German patent DE 4026154) of Bauer invention, anion-exchange membrane by chloromethyl polysulphone through DABCO (1-benzyl-1-azonia-4-azabicyclo[2,2,2]-octane hydroxide) the quaternary ammonium salt amination, regulate the ratio of DABCO and chloromethyl polysulphone, the control degree of cross linking obtains alkali-proof anion-exchange membrane, surface spraying polyethylene yl pyridines and polyacrylic weak solution treat that the solvent evaporation obtains the intermediate layer of the several approximately nanometers of thickness; One deck cation-exchange membrane is scraped on the surface then, and membrane material is a sulfonated polyether-ether-ketone, and in film forming procedure sulfonic group to change the chlorine sulfuryl into crosslinked.
The sandwich construction bipolar membrane of Asahi Glass company invention (day disclosure special permission JP06179757 and JP06298964) needed for three steps just can make, just bipolar membrane material and interlayer structure difference equally.Anion-exchange membrane is mainly quaternised divinylbenzene-styrol copolymer, and minority is quaternized polysulfones; Cation-exchange membrane is a vinylidene type sulfonic acid copolymer, salt such as perhaps corresponding alkaline-earth metal, alkali metal, and the minority film is with the block copolymer of polysulfones and polythiaether.The kind in intermediate layer is more, as product of inorganic ion exchanger, polymer ions exchanger and inorganic ion exchanger and styrene and vinylpyridine etc. etc.
Low resistance, high performance sandwich construction bipolar membrane have been invented by Allied-Signal company (United States Patent (USP) 4116889 and United States Patent (USP) 4766161), anion layer is that styrene-vinyl chloride benzene copolymer obtains through amination, and the cation exchange layer is a sulfonated polystyrene; The intermediate layer be scattered here and there cationic ion-exchange resin, have the anion network polymers structure of the basic group of quaternary ammonium type and non-quaternary ammonium type.
Although adopt the bipolar membrane with " intermediate layer " of three-step approach preparation under high current density, to show low-voltage degradation premium properties with The tape casting, become possibility thereby make bipolar membrane electrodialysis water decomposition process be used for actual industrial process, but existing sandwich construction bipolar membrane and preparation method thereof comes with some shortcomings still.As the difference of negative and positive layer material rerum natura, the negative and positive layer coefficient of expansion differs, and the two-layer physical bond that is generally of negative and positive, and problems such as bonding intensity difference are difficult to guarantee good performance and the stability of bipolar membrane film under the long period of operation condition.Because " intermediate layer " needs independent step to form, its ultra-thinization still awaits improving.
The objective of the invention is to for overcoming the weak point of prior art, a kind of novel bipolar membrane and preparation method thereof is proposed, improve the performance of bipolar membrane from membrane material, membrane structure and film-forming method: make film making process simple than conventional method, the negative and positive two membranes is in conjunction with tight good stability; " intermediate layer " further ultra-thinization makes bipolar membrane have long period of operation stability; Thereby satisfy the demand of practical application in industry better.
Bipolar membrane of the present invention is made up of anion exchange layer, cation exchange layer and intermediate layer.The base material in yin, yang ion exchange layer and intermediate layer is all chloromethyl polysulphone, the about 1.1-3.5 milliequivalent of its chloromethyl content/gram.The intermediate layer is the structure that comprises quaternary ammonium type strong basicity group, non-quaternary ammonium type alkalescent group and sulfonic acid type group.
Bipolar membrane of the present invention, its anion exchange layer can be by the mixture reaction of said chloromethyl polysulphone with excessive amine, diamines, amine and two amine blends or different diamines, cation exchanger resin not, the anti-solvent of anion exchange layer of gained.The cation exchange layer can be made up of the above-mentioned chloromethyl polysulphone of the strongly acidic cation-exchange that is scattered here and there, and the exchange capacity of cationic ion-exchange resin can be 3.0-5.4 milliequivalent/gram, and the resin particle diameter can be 0.01mm-0.1m.Formed intermediate layer can be the cross-linked structure cationic ion-exchange resin that is scattered here and there, that contain quaternary ammonium group, tertiary amine groups.
The present invention also comprises a kind of new film-forming method.Mainly may further comprise the steps: at first make anion-exchange membrane, adopt a step hydrostomia method to form intermediate layer and cation exchange layer simultaneously then with cross-linked structure with excessive diamines and chloromethyl polysulphone reaction.
Anion-exchange membrane is by excessive diamines, such as N, and N-dimethyl-1,3-propane diamine and N, N, N ', N '-tetramethyl-1, (mixed proportion is 1 to the mixed liquor of 6-hexamethylene diamine: 1-6: 1) make the anion-exchange membrane with cross-linked structure with the chloromethyl polysulphone reaction;
On this anion-exchange membrane, adopting the one-step method hydrostomia to contain exchange capacity is 3.0-5.4 milliequivalent/gram, and the resin particle diameter is the chloromethyl polysulphone of 0.01mm-0.1mm, forms not amino-contained, the cation exchange layer of cation exchanger resin only;
Because chloromethyl polysulphone near the anion exchange layer, with amine reaction excessive in the anion exchange layer, and be with a kind of base material, therefore, intermiscibility is good and chemical bond arranged between the yin, yang layer, forms so simultaneously and contains the intermediate layer cationic ion-exchange resin that is scattered here and there, that contain the cross-linked structure of quaternary ammonium group, tertiary amine groups.
Bipolar membrane of the present invention adopts the new filming technology of two step hydrostomias, reduces the thickness in intermediate layer; And use identical yin, yang layer material to improve the caking property and the stability of film; Improve the water decomposition ability of film simultaneously.The intermediate layer is thin, comprises quaternary ammonium type strong basicity group, non-quaternary ammonium type alkalescent group and sulfonic acid type group in the intermediate layer, so the water decomposition ability is good, impedance is low.Prepared bipolar membrane is at 0.5M Na
2SO
4In the aqueous solution, current density 100mA/cm
2Down, pressure drop is less than 2.0V.
Principle of compositionality of the present invention is described in detail as follows:
Bipolar membrane is to be made of the ion exchange layer of two opposite charge or film.Two-layer closely adjacent or be bonded together.Under the effect of DC electric field, water directly is dissociated into hydrogen ion and hydroxide ion, and enters utmost point chamber by the positive and negative ion exchange layer respectively and obtain corresponding bronsted lowry acids and bases bronsted lowry solution.It is 0.022Kwmol that this process is converted into the required energy of hydrogen ion and hydroxide ion to 1 mole of water
-1(25 ℃), hydrolytic dissociation must be reduced to 0.826V by voltage; In fact because the existence of film resistance, boundary layer resistance, actual voltage ratio, theoretical value height.
The core of electrodialytic water decomposing system is a bipolar membrane, and the bipolar membrane of high-quality is the key of this process industrialization.Accompanying drawing 1 shows the bipolar membrane structure and the water decomposition principle of amplifying.Bipolar membrane is a composite membrane 1, is divided into three zones: anion is selected layer 2, cation selective layer 4 and intermediate layer 3.Under galvanic effect, water is dissociated into H in the intermediate layer
+And OH
-Passing the positive and negative ion selects layer to realize the conduction of electricity.Potential drop by bipolar membrane falls summation with the water decomposition potential drop, i.e. E by potential drop, the phase boundary potential of each rete
Always=E
The cavity block layer+ E
The anode membrane layer+ E
The interface+ E
0, E in the formula
0=0.826V (25 ℃).Realize this process for high-efficiency and economic ground, film should have: a) good water permeability in time adds to the intermediate layer with the water that guarantees external solution; B) intermediate layer between the positive and negative layer should be thin as much as possible, to allow H
+And OH
-Effectively transmit.For this reason, bipolar membrane should have special physical arrangement and chemical constitution to satisfy following performance:
1) suitable water decomposition ability
2) low resistance
3) high differential permeability
4) high mechanical strength and long-time stability
The film build method of bipolar membrane mainly is to satisfy its necessary physical arrangement, particularly ultra-thinization in intermediate layer; And the bipolar membrane material mainly is to satisfy its required chemical constitution, comprises yin, yang exchange layer and intermediate layer.
The motion number of ions is inversely proportional in ion-exchange film resistance and the film, depends on the concentration and the degree of dissociation of fixed ion in the film.In order to reduce film resistance, anion, cation in the bipolar membrane need be introduced strong acid, highly basic group, as sulfonate and quaternary ammonium salt.They can dissociate in whole PH scope.During ion exchange capacity 1～2 milliequivalent, the resistivity of highly basic or strong acid amberplex is 50～100 Ω cm on every gram dry film, is 200 μ m as the gross thickness of film, and then total face resistance is 1～2 Ω cm
2
The interface resistance of bipolar membrane depends on the speed of dissociating of interfacial thickness and interfacial water.Interfacial thickness must be thin as far as possible, is generally several nanometers, and will obtain interface resistance this moment is 1～2 Ω cm
2, the water decomposition speed that needs the interface is at least than high by 10 in free solution
6Doubly, it is generally acknowledged, the cation of bipolar membrane boundary layer and anionic group can with water molecule reaction, and the water decomposition reaction mainly appears at the anion-exchange membrane surface, as quaternary ammonium ion, a certain amount of tertiary amine groups can further improve the decomposition rate of water.
The bipolar membrane that this patent adopts two-step method, selects the identical or close yin, yang layer material preparation of performance to have three-decker.At first adopt salivation method to be equipped with solvent-proof anion layer, by of the mixture reaction of above-mentioned chloromethyl polysulphone with excessive amine, diamines, amine and two amine blends or different diamines, cation exchanger resin not, the about 1.1-3.5 milliequivalent of the chloromethyl content/gram of general chloromethyl polysulphone, diamines is generally N, N-dimethyl-1,3-propane diamine and N, N, N ', N '-tetramethyl-1, (mixed proportion is 1 to the mixed liquor of 6-hexamethylene diamine: 1-6: 1) make the anion-exchange membrane with cross-linked structure with the chloromethyl polysulphone reaction; Adopt a step hydrostomia method to form intermediate layer and cation exchange layer simultaneously then, the cation exchange layer is made up of the above-mentioned chloromethyl polysulphone of the strongly acidic cation-exchange that is scattered here and there, the exchange capacity of cationic ion-exchange resin is 3.0-5.4 milliequivalent/gram, and the resin particle diameter is 0.01mm-0.1mm.Formed intermediate layer is cross-linked structure cationic ion-exchange resin, that contain quaternary ammonium group, tertiary amine groups that is scattered here and there.
New filming technology is to allow excessive amine groups and the chloromethyl polysulphone reaction of the second layer form the intermediate layer in the cavity block layer, and this two-step method making plurality of layers of double polarity film has been compared following advantage than conventional method:
1) once film and form intermediate layer and cation selective layer, operation is simple than conventional method;
2) host material of anode membrane layer is a chloromethyl polysulphone, and is identical with the cavity block layer material, and the physical property of two membranes is similar, and has chemical crosslinking between two-layer, so in conjunction with tight good stability; The deficiencies such as long-time stability difference that can avoid two layers of material difference, the coefficient of expansion to differ causing;
3) intermediate layer is thin, comprises quaternary ammonium type strong basicity group, non-quaternary ammonium type alkalescent group and sulfonic acid type group in the intermediate layer, so the water decomposition ability is good, impedance is low.
Polysulfones is a kind of high tenacity, high temperature resistant and membrane material that physical chemistry is stable.The Friedel-Crafts electrophilic substitution reaction under certain condition and certain reagent, very easily takes place in the phenyl ring in the polysulfones (on the bisphenol-A monomer), and as chloromethylation, products obtained therefrom is very important charged membrane material.Chloromethylation products-one chloromethyl polysulphone can react with various amine, forms the amination chloromethyl polysulphone, can be used to do anion-exchange membrane.These films have low resistance and high ion selectivity on the basis of the characteristics that keep original polysulfone material.But the anion exchange layer as bipolar membrane then has higher requirement, must possess excellent solvent-resistance.The present invention is with various diamines, as N, N-dimethyl-1,3-propane diamine and N, N, N ', N '-tetramethyl-1, (mixed proportion is 1 to the mixed liquor of 6-hexamethylene diamine: 1-6: 1), react with chloromethyl polysulphone, the anion-exchange membrane that preparation has cross-linked structure reaches low resistance, high selectivity and good mechanical performance simultaneously to satisfy the solvent resistance that salivation method is equipped with bipolar membrane cavity block layer.
The anion exchange layer goes out the chloromethyl polysulphone amination and obtains.With different diamines, as N, N, N ', N '-tetramethyl-1,6-hexamethylene diamine (TMDAH), be dissolved in the solvent of chloromethylation with chloromethyl polysulphone, as N, N-dimethylacetylamide (DMAc), N, in dinethylformamide (DMF), the dimethyl sulfoxide (DMSO) (DMSO) etc., press the following formula reaction immediately in case mix:
Intermolecular cross-linking can take place in following formula product I or II and another polymer monomer, forms solvent-proof cross-linked structure, and cross-linked structure is as follows:
Diamines still is liquid in a few minutes with after chloromethyl polysulphone mixes.Can be cross-linked to form gel afterwards, gel time is subjected to the influence of chloromethyl content in the type of solvent, temperature, concentration, diamines and the chloromethyl polysulphone.
Any solvent that can dissolve chloromethyl polysulphone can be used as the solvent of preparation bipolar membrane, but best solvent is the solution that chloromethyl polysulphone can be dissolved into homogeneous phase.In general, typical solvent is N, N-dimethylacetylamide (DMAc), N, dinethylformamide (DMF), dimethyl sulfoxide (DMSO) (DMSO) etc.
The concentration range of chloromethyl polysulphone that is used to prepare bipolar membrane anion exchange layer is generally at 10%-22% (percentage by weight).But higher or lower chloromethyl polysulphone concentration also can be used, as long as can not produce serious influence to the performance of telolemma.
Chloromethyl content in the chloromethyl polysulphone is generally at 1.1-3.5 milliequivalent/gram, but is preferably in 2.0-3.0 milliequivalent/gram.
Key of the present invention is once to film to form intermediate layer and cation selective layer.In order to make the intermediate layer ultra-thin, and contain quaternary ammonium type strong basicity group, non-quaternary ammonium type alkalescent group and sulfonic acid type group, chloromethyl polysulphone and excessive amine in the anion exchange layer, diamines, amine reacts with the mixture of two amine blends or different diamines, cation exchanger resin not, diamines is generally N, N-dimethyl-1,3-propane diamine and N, N, N ', N '-tetramethyl-1, (mixed proportion is 1: 1-6: 1) (ratio of chloromethyl and diamines is 1: 1-1: 5) anion-exchange membrane with cross-linked structure is made in reaction to the mixed liquor of 6-hexamethylene diamine with chloromethyl polysulphone; Adopt a step hydrostomia method to form intermediate layer and cation exchange layer simultaneously then, when the chloromethyl polysulphone solution hydrostomia of the strongly acidic cation-exchange that is scattered here and there during to solvent-proof anion exchange layer, the chloromethyl polysulphone of pressing close to the anion exchange layer will react with excessive amine groups, form crosslinking net knot cationic ion-exchange resin, that contain quaternary ammonium group, the tertiary amine groups intermediate layer that is scattered here and there.Like this, have chemical crosslinking between the yin, yang layer, the host material of anode membrane layer is a chloromethyl polysulphone, and is identical with the cavity block layer material, and the physical property of two membranes is similar, so in conjunction with tight good stability; The deficiencies such as long-time stability difference that can avoid two layers of material difference, the coefficient of expansion to differ causing;
Diamines and chloromethyl polysulphone react in solution, solution is coated in forms gel on the glass plate, after 2-10 minute, put into 80-150 ℃ of baking oven and remove solvent about 10-30 minute, make the anion exchange layer of homogeneous phase.The not only anti-solvent of the cavity block layer that makes like this, and chloromethyl content obtains high selectivity in type by control temperature, concentration, diamines and the chloromethyl polysulphone.The thickness of film is generally 20-80 μ m.
Then, at the direct curtain coating one deck anode membrane liquid in the surface of anion-exchange membrane.The second layer is to be the solution of the chloromethyl polysulphone of cationic ion-exchange resin 0.01 gram-0.2 gram of the 0.01-0.2mm 10%-20% (percentage by weight) that is dissolved in 10-30ml with average grain diameter, and dry 5～50min makes in 80-150 ℃ baking oven.The exchange capacity of cationic ion-exchange resin is 3.0-5.4 milliequivalent/gram.
The prepared bipolar membrane of the present invention is at 0.5M Na
2SO
4In the aqueous solution, current density 100mA/cm
2Down, pressure drop is less than 2.0V.Measuring media is 0.5MNa
2SO
4Solution is pressed on the both sides of bipolar membrane with uncorruptible platinized platinum electrode, connects the voltage that platinized platinum is measured the film both sides with universal meter, and with ammeter read current size.Change electric current and measure the situation of voltage change.Used bipolar membrane effective area A=100cm
2, then
Current density i (mA/cm
2)=electric current I (mA)/effective film area A (cm
2).
Fig. 1 is bipolar membrane structure and water decomposition principle schematic.
Following embodiment is used for illustrating technical scope of the present invention, but is not limited thereto.
Embodiment 1.
The preparation of bipolar membrane is dissolved in the 2g chloromethyl polysulphone among the 15mlDMF according to the following steps, adds 2mlN, N, and N ', N '-tetramethyl-1, the 6-hexamethylene diamine stirs, casting film-forming.Put into 125 ℃ of baking oven 8～20min, after question response fully and the solvent major part removes, directly be coated with the second layer.The second layer is the solution that average grain diameter is uniformly dispersed in chloromethyl polysulphone for the 0.02mm cationic ion-exchange resin.Glass plate is put into 125 ℃ of baking oven 8～15min once more, and cooling promptly gets bipolar membrane.This film is at 0.5M Na
2SO
4In the aqueous solution, current density 100mA/cm
2Down, pressure drop is less than 4.1V.
Embodiment 2
The preparation of bipolar membrane is dissolved in the 2g chloromethyl polysulphone among the 15mlDMF according to the following steps, adds hybrid diamine N, N-dimethyl-1,3-propane diamine and N, N, N ', N '-tetramethyl-1,6-hexamethylene diamine (mol ratio DMAPA: TMDAH is 3: 1) 2.23g replaces N, N, N ', N '-tetramethyl-1,6-hexamethylene diamine, stir casting film-forming.Put into 125 ℃ of baking oven 8～20min, after question response fully and the solvent major part removes, directly be coated with the second layer.The second layer is the solution that average grain diameter is uniformly dispersed in chloromethyl polysulphone for the 0.02mm cationic ion-exchange resin.Glass plate is put into 125 ℃ of baking oven 8～15min once more, and cooling promptly gets bipolar membrane.This film is at 0.5M Na
2SO
4In the aqueous solution, current density 100mA/cm
2Down, pressure drop is less than 2.0V.
Embodiment 3
The preparation of bipolar membrane is dissolved in the 2g chloromethyl polysulphone among the 15mlDMF according to the following steps, adds hybrid diamine N, N-dimethyl-1,3-propane diamine and N, N, N ', N '-tetramethyl-1,6-hexamethylene diamine (mol ratio DMAPA: TMDAH is 3: 1) 2.23g replaces N, N, N ', N '-tetramethyl-1,6-hexamethylene diamine, stir casting film-forming.Put into 125 ℃ of baking oven 8～20min, after question response fully and the solvent major part removes, directly be coated with the second layer.The second layer is the solution that average grain diameter is uniformly dispersed in chloromethyl polysulphone for the 0.04mm cationic ion-exchange resin.Glass plate is put into 125 ℃ of baking oven 8～15min once more, and cooling promptly gets bipolar membrane.This film is at 0.5M Na
2SO
4In the aqueous solution, current density 100mA/cm
2Down, pressure drop is less than 5.0V.234567890
Claims (6)
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|---|---|---|---|
| CN99125066A CN1101254C (en) | 1999-11-26 | 1999-11-26 | Bipolar film and its preparing process |
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|---|---|---|---|
| CN99125066A CN1101254C (en) | 1999-11-26 | 1999-11-26 | Bipolar film and its preparing process |
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| CN1250681A true CN1250681A (en) | 2000-04-19 |
| CN1101254C CN1101254C (en) | 2003-02-12 |
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ID=5283710
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Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1323745C (en) * | 2004-06-01 | 2007-07-04 | 中国科学技术大学 | Bipolar film and preparation method thereof |
| CN102838747A (en) * | 2012-08-29 | 2012-12-26 | 南京理工大学 | Preparation method of side chain crosslinked polymer and side chain crosslinked polymer anion exchange membrane of side chain crosslinked polymer |
| CN106323689A (en) * | 2016-08-22 | 2017-01-11 | 中国食品发酵工业研究院 | Water quality monitoring-orientated polar organic trace pollutant trap |
| CN107227465A (en) * | 2016-03-23 | 2017-10-03 | 北京汇益科技股份有限公司 | A kind of method and its equipment of the bipolar film preparation soda acid of nanofiber |
| CN110461916A (en) * | 2017-03-28 | 2019-11-15 | 豪威株式会社 | Bipolar ion-exchange membrane using heterogeneous ion-exchange membrane carrier and its manufacturing method |
| CN110756055A (en) * | 2019-05-15 | 2020-02-07 | 北京化工大学 | Bipolar membrane and preparation method thereof |
| CN112752610A (en) * | 2018-09-25 | 2021-05-04 | 懿华水处理技术有限责任公司 | Monovalent selective cation exchange membranes |
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| CN119565392A (en) * | 2024-11-20 | 2025-03-07 | 万华化学集团股份有限公司 | A bipolar membrane and its preparation and use method |
| CN119812416A (en) * | 2024-12-30 | 2025-04-11 | 苏州科润新材料股份有限公司 | Composite ion exchange membrane and preparation method and application thereof |
Family Cites Families (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4116889A (en) * | 1976-08-19 | 1978-09-26 | Allied Chemical Corporation | Bipolar membranes and method of making same |
| US4766161A (en) * | 1986-06-05 | 1988-08-23 | Allied Corporation | Bipolar membranes and methods of making same |
| JPH0813900B2 (en) * | 1988-12-19 | 1996-02-14 | 株式会社トクヤマ | Bipolar film manufacturing method |
| JP2801469B2 (en) * | 1992-07-07 | 1998-09-21 | 株式会社トクヤマ | Bipolar membrane |
-
1999
- 1999-11-26 CN CN99125066A patent/CN1101254C/en not_active Expired - Fee Related
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1323745C (en) * | 2004-06-01 | 2007-07-04 | 中国科学技术大学 | Bipolar film and preparation method thereof |
| CN102838747A (en) * | 2012-08-29 | 2012-12-26 | 南京理工大学 | Preparation method of side chain crosslinked polymer and side chain crosslinked polymer anion exchange membrane of side chain crosslinked polymer |
| CN107227465A (en) * | 2016-03-23 | 2017-10-03 | 北京汇益科技股份有限公司 | A kind of method and its equipment of the bipolar film preparation soda acid of nanofiber |
| CN106323689A (en) * | 2016-08-22 | 2017-01-11 | 中国食品发酵工业研究院 | Water quality monitoring-orientated polar organic trace pollutant trap |
| CN106323689B (en) * | 2016-08-22 | 2020-02-21 | 中国食品发酵工业研究院有限公司 | A Water Quality Monitoring-Oriented Trap for Trace Polar Organic Pollutants |
| CN110461916A (en) * | 2017-03-28 | 2019-11-15 | 豪威株式会社 | Bipolar ion-exchange membrane using heterogeneous ion-exchange membrane carrier and its manufacturing method |
| CN112752610A (en) * | 2018-09-25 | 2021-05-04 | 懿华水处理技术有限责任公司 | Monovalent selective cation exchange membranes |
| CN112752610B (en) * | 2018-09-25 | 2024-02-13 | 懿华水处理技术有限责任公司 | Monovalent selective cation exchange membrane |
| CN110756055A (en) * | 2019-05-15 | 2020-02-07 | 北京化工大学 | Bipolar membrane and preparation method thereof |
| CN117285752A (en) * | 2023-02-01 | 2023-12-26 | 张大庆 | Synthesis method and application of degradable chitosan composite membrane material |
| CN119565392A (en) * | 2024-11-20 | 2025-03-07 | 万华化学集团股份有限公司 | A bipolar membrane and its preparation and use method |
| CN119812416A (en) * | 2024-12-30 | 2025-04-11 | 苏州科润新材料股份有限公司 | Composite ion exchange membrane and preparation method and application thereof |
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